EP2585499A1 - Catalyst system for the polymerization of olefins - Google Patents
Catalyst system for the polymerization of olefinsInfo
- Publication number
- EP2585499A1 EP2585499A1 EP11723083.9A EP11723083A EP2585499A1 EP 2585499 A1 EP2585499 A1 EP 2585499A1 EP 11723083 A EP11723083 A EP 11723083A EP 2585499 A1 EP2585499 A1 EP 2585499A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- hydrogen
- groups
- bis
- catalyst
- dimethoxypropane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/647—Catalysts containing a specific non-metal or metal-free compound
- C08F4/649—Catalysts containing a specific non-metal or metal-free compound organic
- C08F4/6494—Catalysts containing a specific non-metal or metal-free compound organic containing oxygen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/04—Monomers containing three or four carbon atoms
- C08F10/06—Propene
Definitions
- the present invention relates to a catalyst system capable to show, in propylene polymerization, high activity, stereospecificity and increased hydrogen response.
- Catalyst systems for the stereospecific polymerization of olefins are widely known in the art.
- the most common type of catalyst system belongs to the Ziegler-Natta family and comprises a solid catalyst component, constituted by a magnesium dihalide on which are supported a titanium compound and an internal electron donor compound, used in combination with an Al-alkyl compound.
- an external donor usually an alkylalkoxysilane, is needed in order to obtain higher isotacticity.
- an external donor is absent, the isotactic index of the resulting polymer is not sufficiently high even if a 1,3-diether is used as internal donor.
- TWIM thin wall injection molding
- the low molecular weight polymers are commonly obtained by increasing the content of the chain transfer agent (molecular weight regulator) in particular hydrogen which is commonly used industrially.
- catalysts having high hydrogen response are the Ziegler-Natta catalysts containing 1,3-diethers described for example in EP622380. Such catalysts components are generally able to produce propylene polymers with high melt flow rates. When an external donor of the alkylalkoxysilane type is added in order to increase its stereospecificity, the hydrogen response of the catalyst is lowered.
- a catalyst system comprising the product obtained by contacting (a) a solid catalyst component containing Mg, Ti, halogen and at least an electron donor compound selected from 1,3- diethers;
- the solid catalyst component comprises Mg, Ti, halogen and an electron donor selected from 1,3-diethers of formula (I):
- R 1 and R n are the same or different and are hydrogen or linear or branched Ci-Cis hydrocarbon groups which can also form one or more cyclic structures;
- R m groups, equal or different from each other, are hydrogen or Ci-Cig hydrocarbon groups;
- R ⁇ groups equal or different from each other, have the same meaning of R m except that they cannot be hydrogen;
- each of R 1 to R ⁇ groups can contain heteroatoms selected from halogens, N, O, S and Si.
- R ⁇ is a 1-6 carbon atom alkyl radical and more particularly a methyl while the R m radicals are preferably hydrogen.
- R n can be ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, isopentyl, 2-ethylhexyl, cyclopentyl, cyclohexyl, methylcyclohexyl, phenyl or benzyl;
- R n when R 1 is hydrogen, R n can be ethyl, butyl, sec-butyl, tert-butyl, 2-ethylhexyl, cyclohexylethyl, diphenylmethyl, p-chlorophenyl, 1-naphthyl, 1-decahydronaphthyl;
- ethers that can be advantageously used include: 2-(2-ethylhexyl)l,3- dimethoxypropane, 2-isopropyl-l,3-dimethoxypropane, 2-butyl-l,3-dimethoxypropane, 2- sec-butyl- 1 ,3-dimethoxypropane, 2-cyclohexyl- 1 ,3-dimethoxypropane, 2-phenyl- 1 ,3- dimethoxypropane, 2-tert-butyl-l,3-dimethoxypropane, 2-cumyl-l,3-dimethoxypropane, 2- (2-phenylethyl)- 1 ,3-dimethoxypropane, 2-(2-cyclohexylethyl)- 1 ,3-dimethoxypropane, 2-(p- chlorophenyl)- 1 ,3-dimethoxypropane, 2-(diphenylmethyl)- 1
- radicals R have the same meaning explained above and the radicals R and R , equal or different to each other, are selected from the group consisting of hydrogen; halogens, preferably CI and F; Ci-C 2 o alkyl radicals, linear or branched; C 3 -C 2 o cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals and two or more of the R v radicals can be bonded to each other to form condensed cyclic structures, saturated or unsaturated, optionally substituted with R VI radicals selected from the group consisting of halogens, preferably CI and F; C1-C2 0 alkyl radicals, linear or branched; C3-C2 0 cycloalkyl, C 6 -C 2 o aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals; said radicals R v and R VI optional
- all the R m radicals are hydrogen, and all the R ⁇ radicals are methyl.
- the 1,3-diethers of formula (II) in which two or more of the R v radicals are bonded to each other to form one or more condensed cyclic structures, preferably benzenic, optionally substituted by R VI radicals.
- Specially preferred are the compounds of formula (III):
- R VI radicals equal or different are hydrogen; halogens, preferably CI and F; Q- C 2 o alkyl radicals, linear or branched; C3-C20 cycloalkyl, C 6 -C 2 o aryl, C7-C20 alkylaryl and C7-C2 0 arylalkyl radicals, optionally containing one or more heteroatoms selected from the group consisting of N, 0, S, P, Si and halogens, in particular CI and F, as substitutes for carbon or hydrogen atoms, or both; the radicals R m and R ⁇ are as defined above for formula (II).
- the solid catalyst component (a) can also contain additional electron donors belonging to ethers, esters of aromatic or aliphatic mono or dicarboxylic acids, ketones, or alkoxyesters.
- additional donors belonging to ethers, esters of aromatic or aliphatic mono or dicarboxylic acids, ketones, or alkoxyesters.
- the additional donors may be present in an amount such that the 1,3-diether/other donor molar ratio ranges from 0.1 to 10 preferably from 0.2 to 8.
- the catalyst components of the invention comprise, in addition to the above electron donors, Ti, Mg and halogen.
- the catalyst components comprise a titanium compound, having at least a Ti-halogen bond and the above mentioned electron donor compounds supported on a Mg halide.
- the magnesium halide is preferably MgC . in active form which is widely known from the patent literature as a support for Ziegler-Natta catalysts. Patents USP 4,298,718 and USP 4,495,338 were the first to describe the use of these compounds in Ziegler-Natta catalysis.
- magnesium dihalides in active form used as support or co-support in components of catalysts for the polymerization of olefins are characterized by X-ray spectra in which the most intense diffraction line that appears in the spectrum of the non-active halide is diminished in intensity and is replaced by a halo whose maximum intensity is displaced towards lower angles relative to that of the more intense line.
- the preferred titanium compounds used in the catalyst component of the present invention are TiCk and TiCk; furthermore, also Ti-haloalcoholates of formula Ti(OR) n - y X y can be used, where n is the valence of titanium, y is a number between 1 and n-1, X is halogen and R is a hydrocarbon radical having from 1 to 10 carbon atoms.
- the preparation of the solid catalyst component can be carried out according to several methods. According to one of these methods, the magnesium dichloride in an anhydrous state, the titanium compound and the electron donor compounds are milled together under conditions in which activation of the magnesium dichloride occurs. The so obtained product can be treated one or more times with an excess of TiCl 4 at a temperature between 80 and 135°C. This treatment is followed by washings with hydrocarbon solvents until chloride ions have disappeared. According to a further method, the product obtained by co-milling the magnesium chloride in an anhydrous state, the titanium compound and the electron donor compounds are treated with halogenated hydrocarbons such as 1,2- dichloroethane, chlorobenzene, dichloromethane etc.
- halogenated hydrocarbons such as 1,2- dichloroethane, chlorobenzene, dichloromethane etc.
- the treatment is carried out for a time between 1 and 4 hours and at temperature of from 40°C to the boiling point of the halogenated hydrocarbon.
- the product obtained is then generally washed with inert hydrocarbon solvents such as hexane.
- magnesium dichloride is preactivated according to well known methods and then treated with an excess of TiCU at a temperature of about 80 to 135°C in the presence of the electron donor compounds.
- a further method described in WO2005/095472 comprises reacting, in the presence of a 1,3-diether, a titanium compound having at least Ti-Cl bond with a precursor of formula MgCl n (OR) 2 - n LB p in which n is from 0.1 to 1.9, p is higher than 0.4, and R is a CI -CI 5 hydrocarbon group.
- the reaction is carried out in and an excess of TiCU at a temperature of about 80 to 120°C.
- the solid catalyst component can be prepared by reacting a titanium compound of formula Ti(OR) n - y X y , where n is the valence of titanium and y is a number between 1 and n, preferably TiCU, with a magnesium chloride deriving from an adduct of formula MgCUpROH, where p is a number between 0.1 and 6, preferably from 2 to 3.5, and R is a hydrocarbon radical having 1-18 carbon atoms.
- the adduct can be suitably prepared in spherical form by mixing alcohol and magnesium chloride in the presence of an inert hydrocarbon immiscible with the adduct, operating under stirring conditions at the melting temperature of the adduct (100-130°C). Then, the emulsion is quickly quenched, thereby causing the solidification of the adduct in form of spherical particles. Examples of spherical adducts prepared according to this procedure are described in USP 4,399,054 and USP 4,469,648.
- the so obtained adduct can be directly reacted with Ti compound or it can be previously subjected to thermal controlled dealcoholation (80- 130°C) so as to obtain an adduct in which the number of moles of alcohol is generally lower than 3 preferably between 0.1 and 2.5.
- the reaction with the Ti compound can be carried out by suspending the adduct (dealcoholated or as such) in cold TiCU (generally 0°C); the mixture is heated up to 80-130°C and kept at this temperature for 0.5-2 hours.
- the treatment with TiCU can be carried out one or more times.
- the electron donor compounds can be added during the treatment with TiCU- They can be added together in the same treatment with TiCU or separately in two or more treatments.
- the preparation of catalyst components in spherical form are described for example in European Patent Applications EP-A-395083, EP-A-553805, EP-A-553806, EPA601525 and WO98/44001.
- the solid catalyst components obtained according to the above method show a surface area (by B.E.T. method) generally between 20 and 500 m 2 /g and preferably between 50 and 400 m 2 /g, and a total porosity (by B.E.T. method) higher than 0.2 cm 3 /g preferably between 0.2 and 0.6 cm 3 /g.
- the porosity (Hg method) due to pores with radius up to ⁇ . ⁇ generally ranges from 0.3 to 1.5 cffiVg, preferably from 0.45 to 1 cffiVg.
- the solid catalyst component has an average particle size ranging from 5 to 120 ⁇ and more preferably from 10 to 100 ⁇ .
- the alkyl-Al compound (b) is preferably selected from the trialkyl aluminum compounds such as for example triethylaluminum, triisobutylaluminum, tri-n-butylaluminum, tri-n-hexylaluminum, tri- n-octylaluminum. It is also possible to use mixtures of trialtylaluminum's with al laluminum halides, alkylaluminum hydrides or alkylaluminum sesquichlorides such as AlEt 2 Cl and Al 2 Et 3 Cl3.
- the ester (c) is used as external electron donor and is preferably selected from the compounds in which R is a C1-C6 linear or branched alkyl, preferably ethyl or isobutyl.
- n is preferably from 2 to 7, more preferably from 4 to 6 and especially from 4 to 5.
- esters (c) are diethyl succinate, diethyl glutarate, diethyl adipate, diethyl suberate, diethyl pimelate and the corresponding esters deriving from substitution of ethyl with methyl, isobutyl, or 2-ethylhexyl.
- R is hydrogen or a CI -CIO hydrocarbon group or mixtures of such olefins.
- it is particularly suited for the preparation of propylene polymers due to the fact that it shows increased hydrogen response with respect to the most common used alkylalkoxysilane, while maintaining high stereospecificity expressed by a percentage of xylene insolubility at 25°C generally of 97% or higher.
- the Molecular Weight Distribution (expressed as polydispersity index determined as described hereinafter) remains narrow, generally lower than 4 and preferably lower than or equal to 3.5. Another important advantage is that hydrogen response and high stereospecificity are retained while maintaining a very good level of polymerization activity.
- any kind of polymerization process can be used with the catalysts of the invention that are very versatile.
- the polymerization can be carried out for example in slurry using as diluent a liquid inert hydrocarbon, or in bulk using the liquid monomer (propylene) as a reaction medium, or in solution using either monomers or inert hydrocarbons as solvent for the nascent polymer.
- the process of the present invention is particularly advantageous for producing said isotactic propylene polymers with high fluidity in liquid phase because in such a type of process the pressure problems connected to the use of increased amounts of hydrogen is more evident.
- the liquid phase process can be either in slurry, solution or bulk (liquid monomer). This latter technology is the most preferred and can be carried out in various types of reactors such as continuous stirred tank reactors, loop reactors or plug-flow ones.
- the polymerization is generally carried out at temperature of from 20 to 120°C, preferably of from 40 to 85°C.
- the operating pressure is generally between 0.5 and 10 MPa, preferably between 1 and 5 MPa.
- the operating pressure is generally between 1 and 6 MPa preferably between 1.5 and 4 MPa.
- the catalyst of the present invention can be used as such in the polymerization process by introducing it directly into the reactor.
- the catalyst can be pre- polymerized before being introduced into the first polymerization reactor.
- pre- polymerized means a catalyst which has been subject to a polymerization step at a low conversion degree.
- a catalyst is considered to be pre-polymerized when the amount the polymer produced is from about 0.1 up to about 1000 g per gram of solid catalyst component.
- the pre-polymerization can be carried out with the a-olefms selected from the same group of olefins disclosed before.
- the conversion of the pre-polymerized catalyst component is from about 0.2 g up to about 500 g per gram of solid catalyst component.
- the pre-polymerization step can be carried out at temperatures from 0 to 80°C preferably from 5 to 50°C in liquid or gas-phase.
- the pre-polymerization step can be performed in-line as a part of a continuous polymerization process or separately in a batch process.
- the batch pre-polymerization of the catalyst of the invention with ethylene in order to produce an amount of polymer ranging from 0.5 to 20 g per gram of catalyst component is particularly preferred.
- microspheroidal MgCl 2 -2.8C 2 H 5 OH was prepared according to the method described in ex.2 of WO98/44009 but operating on larger scale.
- the solid adduct so obtained were then subject to thermal dealcoholation at increasing temperatures from 30 to 130°C and operating in nitrogen current until reaching an alcohol content of 2.1 moles per mol of MgCl 2 .
- the solid was washed with anhydrous hexane six times (6 x 100 ml) in temperature gradient down to 60°C and one time (100 ml) at room temperature. The solid was finally dried under vacuum and analyzed. The amount of Ti bonded on the catalyst resulted in 3.9%wt., while the amount of internal donor bonded resulted in 12%wt.
- the temperature was raised to 100°C and maintained for 1 hour. Thereafter, stirring was stopped, the solid product was allowed to settle and the supernatant liquid was siphoned off maintaining the temperature at 100°C. After the supernatant was removed, additional 250 ml of fresh TiCU were added. The mixture was then heated at 110°C and kept at this temperature for 60 minutes. Once again the stirring was interrupted; the solid product was allowed to settle and the supernatant liquid was siphoned off maintaining the temperature at 110°C. A third aliquot of fresh TiCU (250 ml) was added, the mixture was maintained under agitation at 110°C for 30 minutes and then the supernatant liquid was siphoned off.
- the solid was washed with anhydrous hexane six times (6 x 100 ml) in temperature gradient down to 60°C and one time (100 ml) at room temperature. The solid was finally dried under vacuum and analyzed.
- the amount of Ti bonded on the catalyst resulted in 3.7%wt., while the amount of internal donors bonded resulted in 2.8%wt. for 9,9-bis(methoxymethyl)fluorene and 8.7%wt. for diethyl 2,3- diisopropylsuccinate.
- DIPS Diethyl 2,3-diisopropylsuccinate
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Emergency Medicine (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP11723083.9A EP2585499B1 (en) | 2010-06-24 | 2011-06-06 | Catalyst system for the polymerization of olefins |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10167165 | 2010-06-24 | ||
US39865410P | 2010-06-29 | 2010-06-29 | |
EP11723083.9A EP2585499B1 (en) | 2010-06-24 | 2011-06-06 | Catalyst system for the polymerization of olefins |
PCT/EP2011/059267 WO2011160936A1 (en) | 2010-06-24 | 2011-06-06 | Catalyst system for the polymerization of olefins |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2585499A1 true EP2585499A1 (en) | 2013-05-01 |
EP2585499B1 EP2585499B1 (en) | 2019-02-27 |
Family
ID=44477662
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11723083.9A Active EP2585499B1 (en) | 2010-06-24 | 2011-06-06 | Catalyst system for the polymerization of olefins |
Country Status (5)
Country | Link |
---|---|
US (1) | US20130102744A1 (en) |
EP (1) | EP2585499B1 (en) |
CN (1) | CN102958953B (en) |
BR (1) | BR112012033011B1 (en) |
WO (1) | WO2011160936A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113754804A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system for olefin polymerization and application thereof |
CN113754803A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system and application thereof as catalyst for olefin polymerization |
CN113754799A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Solid catalyst component and solid catalyst system containing same |
CN113754802A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system for olefin polymerization reaction and prepolymerization catalyst composition |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2624923T3 (en) * | 2011-04-12 | 2017-07-18 | Basell Poliolefine Italia S.R.L. | Catalyst components for the polymerization of olefins |
ES2651456T3 (en) | 2013-08-14 | 2018-01-26 | Borealis Ag | Propylene composition with better low temperature impact resistance |
BR112016002682A8 (en) | 2013-08-21 | 2020-01-28 | Borealis Ag | high flow polyolefin composition with high rigidity and toughness |
WO2015024887A1 (en) | 2013-08-21 | 2015-02-26 | Borealis Ag | High flow polyolefin composition with high stiffness and toughness |
EP2853563B1 (en) | 2013-09-27 | 2016-06-15 | Borealis AG | Films suitable for BOPP processing from polymers with high XS and high Tm |
CN104513332B (en) * | 2013-09-30 | 2017-06-06 | 中国石油化工股份有限公司 | Catalyst system and its application for olefinic polymerization |
CN104513331B (en) * | 2013-09-30 | 2017-06-06 | 中国石油化工股份有限公司 | Carbon monoxide-olefin polymeric and its application for olefinic polymerization |
CN104513328B (en) * | 2013-09-30 | 2017-09-29 | 中国石油化工股份有限公司 | Carbon monoxide-olefin polymeric and its application for olefinic polyreaction |
TWI639626B (en) * | 2013-09-30 | 2018-11-01 | 中國石油化工科技開發有限公司 | Catalyst composition for olefin polymerization and application thereof |
EP2860031B1 (en) | 2013-10-11 | 2016-03-30 | Borealis AG | Machine direction oriented film for labels |
WO2015059229A1 (en) | 2013-10-24 | 2015-04-30 | Borealis Ag | Low melting pp homopolymer with high content of regioerrors and high molecular weight |
EP2865713B1 (en) | 2013-10-24 | 2016-04-20 | Borealis AG | Blow molded article based on bimodal random copolymer |
CN105722869B (en) | 2013-10-29 | 2017-09-12 | 北欧化工公司 | Solid single-point catalyst with high polymerization activity |
ES2644829T3 (en) | 2013-11-22 | 2017-11-30 | Borealis Ag | Low emission propylene homopolymer with high melt flow |
BR112016011829B1 (en) * | 2013-12-04 | 2022-01-18 | Borealis Ag | COMPOSITION OF POLYPROPYLENE, FIBER AND MELT BLOWN, ARTICLE AND USE OF POLYPROPYLENE COMPOSITION |
KR101873134B1 (en) | 2013-12-18 | 2018-06-29 | 보레알리스 아게 | Bopp film with improved stiffness/toughness balance |
EP3094660B1 (en) | 2014-01-17 | 2018-12-19 | Borealis AG | Process for preparing propylene/1-butene copolymers |
JP6474417B2 (en) | 2014-02-06 | 2019-02-27 | ボレアリス エージー | Soft and transparent impact copolymers |
CN112225997B (en) | 2014-02-06 | 2023-09-22 | 北欧化工公司 | High impact strength flexible copolymers |
EP2907841A1 (en) | 2014-02-14 | 2015-08-19 | Borealis AG | Polypropylene composite |
EP2947118B1 (en) | 2014-05-20 | 2017-11-29 | Borealis AG | Polypropylene composition for automotive interior applications |
US10633463B2 (en) * | 2015-12-31 | 2020-04-28 | Braskem America, Inc. | Non-phthalate catalyst system and its use in the polymerization of olefins |
WO2019094216A1 (en) | 2017-11-13 | 2019-05-16 | W.R. Grace & Co.-Conn. | Catalyst components for propylene polymerization |
US20220298272A1 (en) * | 2019-09-17 | 2022-09-22 | Basell Poliolefine Italia S.R.L. | Catalyst components for the polymerization of olefins |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3401157A (en) * | 1967-02-21 | 1968-09-10 | Eastman Kodak Co | Three-component aluminum-titanium tetrahalide catalysts for olefin polymerization |
DK133012C (en) | 1968-11-21 | 1976-08-09 | Montedison Spa | CATALYST FOR POLYMERIZATION OF ALKENES |
YU35844B (en) | 1968-11-25 | 1981-08-31 | Montedison Spa | Process for obtaining catalysts for the polymerization of olefines |
IT1096661B (en) | 1978-06-13 | 1985-08-26 | Montedison Spa | PROCEDURE FOR THE PREPARATION OF SOLID SPHEROIDAL PRODUCTS AT AMBIENT TEMPERATURE |
IT1098272B (en) | 1978-08-22 | 1985-09-07 | Montedison Spa | COMPONENTS, CATALYSTS AND CATALYSTS FOR THE POLYMERIZATION OF ALPHA-OLEFINS |
IT1230134B (en) | 1989-04-28 | 1991-10-14 | Himont Inc | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE. |
IT1262934B (en) | 1992-01-31 | 1996-07-22 | Montecatini Tecnologie Srl | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE |
IT1262935B (en) | 1992-01-31 | 1996-07-22 | Montecatini Tecnologie Srl | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE |
IT1256648B (en) | 1992-12-11 | 1995-12-12 | Montecatini Tecnologie Srl | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINS |
CA2121721C (en) | 1993-04-29 | 2004-11-23 | Giampiero Morini | Crystalline propylene polymers having high melt flow rate values and a narrow molecular weight distribution |
AUPO591797A0 (en) | 1997-03-27 | 1997-04-24 | Commonwealth Scientific And Industrial Research Organisation | High avidity polyvalent and polyspecific reagents |
ATE259832T1 (en) | 1997-03-29 | 2004-03-15 | Basell Poliolefine Spa | MAGNESIUM DIHALOGENIDE/ALCOHOL ADDUCTS, METHOD FOR THE PRODUCTION THEREOF AND CATALYST COMPONENTS PRODUCED THEREFROM |
ES2212560T3 (en) * | 1998-05-06 | 2004-07-16 | Basell Poliolefine Italia S.P.A. | CATALYZING COMPONENTS FOR POLYMERIZATION OF OLEFINS. |
ATE335014T1 (en) * | 1999-04-15 | 2006-08-15 | Basell Poliolefine Srl | COMPONENTS AND CATALYSTS FOR OLEFIN POLYMERIZATION |
KR20070011378A (en) | 2004-03-29 | 2007-01-24 | 바셀 폴리올레핀 이탈리아 에스.알.엘 | Magnesium chloride-based adducts and catalyst components obtained therefrom |
KR101787927B1 (en) * | 2007-12-21 | 2017-10-18 | 더블유.알. 그레이스 앤드 캄파니-콘. | Self-limiting catalyst composition with bidentate internal donor |
-
2011
- 2011-06-06 WO PCT/EP2011/059267 patent/WO2011160936A1/en active Application Filing
- 2011-06-06 CN CN201180031051.5A patent/CN102958953B/en active Active
- 2011-06-06 US US13/806,641 patent/US20130102744A1/en not_active Abandoned
- 2011-06-06 BR BR112012033011-0A patent/BR112012033011B1/en active IP Right Grant
- 2011-06-06 EP EP11723083.9A patent/EP2585499B1/en active Active
Non-Patent Citations (1)
Title |
---|
See references of WO2011160936A1 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113754804A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system for olefin polymerization and application thereof |
CN113754803A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system and application thereof as catalyst for olefin polymerization |
CN113754799A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Solid catalyst component and solid catalyst system containing same |
CN113754802A (en) * | 2020-06-05 | 2021-12-07 | 中国石油化工股份有限公司 | Catalyst system for olefin polymerization reaction and prepolymerization catalyst composition |
CN113754803B (en) * | 2020-06-05 | 2023-02-24 | 中国石油化工股份有限公司 | Catalyst system and application thereof as catalyst for olefin polymerization |
Also Published As
Publication number | Publication date |
---|---|
BR112012033011B1 (en) | 2020-05-26 |
US20130102744A1 (en) | 2013-04-25 |
WO2011160936A1 (en) | 2011-12-29 |
CN102958953B (en) | 2015-08-05 |
BR112012033011A2 (en) | 2016-12-20 |
EP2585499B1 (en) | 2019-02-27 |
CN102958953A (en) | 2013-03-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2585499B1 (en) | Catalyst system for the polymerization of olefins | |
AU759295B2 (en) | Catalyst components for the polymerization of olefins | |
US8062989B2 (en) | Magnesium chloroakolate-based catalyst precursors | |
US7560521B2 (en) | Components and catalysts for the polymerization of olefins | |
US9593171B2 (en) | Catalyst components for the polymerization of olefins | |
EP2225287A1 (en) | Catalyst components for the polymerization of olefins | |
EP2630170B1 (en) | Catalyst system for the polymerization of olefins | |
US7932206B2 (en) | Magnesium dichloride-based adducts and catalyst components obtained therefrom | |
US20070282147A1 (en) | Magnesium Chloride-Based Adducts And Catalyst Components Obtained Therefrom | |
US8835578B2 (en) | Catalyst components for the polymerization of olefins | |
WO2013092205A1 (en) | Catalyst system for the polymerization of olefins | |
ES2717176T3 (en) | Catalyst system for the polymerization of olefins | |
MXPA00000270A (en) | Catalyst components for the polymerization of olefins |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20121116 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
DAX | Request for extension of the european patent (deleted) | ||
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R079 Ref document number: 602011056592 Country of ref document: DE Free format text: PREVIOUS MAIN CLASS: C08F0010060000 Ipc: C08F0110060000 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C08F 4/649 20060101ALI20170208BHEP Ipc: C08F 4/651 20060101ALI20170208BHEP Ipc: C08F 10/06 20060101ALI20170208BHEP Ipc: C08F 110/06 20060101AFI20170208BHEP |
|
17Q | First examination report despatched |
Effective date: 20170303 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: BASELL POLIOLEFINE ITALIA S.R.L. |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: BASELL POLIOLEFINE ITALIA S.R.L. |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20180921 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1101200 Country of ref document: AT Kind code of ref document: T Effective date: 20190315 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602011056592 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2717176 Country of ref document: ES Kind code of ref document: T3 Effective date: 20190619 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20190227 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190627 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190527 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20190415 Year of fee payment: 13 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190528 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190527 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190627 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20190612 Year of fee payment: 9 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602011056592 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
26N | No opposition filed |
Effective date: 20191128 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20190606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20190630 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: UEP Ref document number: 1101200 Country of ref document: AT Kind code of ref document: T Effective date: 20190227 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190606 Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190630 Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190630 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190630 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190630 |
|
REG | Reference to a national code |
Ref country code: FI Ref legal event code: MAE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200606 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 1101200 Country of ref document: AT Kind code of ref document: T Effective date: 20200606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20110606 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20190227 |
|
P01 | Opt-out of the competence of the unified patent court (upc) registered |
Effective date: 20230414 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20230509 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20230703 Year of fee payment: 13 |